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METHOD FOR PRODUCING DIESEL FUEL FROM SOLID synthetic hydrocarbons obtained by the Fischer-Tropsch synthesis, and catalysts FOR ITS IMPLEMENTATION

机译:由费-托合成获得的固体合成烃生产柴油的方法及其实施催化剂

摘要

FIELD: machine building.;SUBSTANCE: method for obtaining diesel fuel from solid synthetic hydrocarbons obtained as per Fischer-Tropsch method is described. It involves hydrocracking/isodewaxing of solid hydrocarbons on a catalyser containing a carrier and a plate; at that, the carrier is made from mixture of 10-40% zeolite SAPO-41 and γ-Al2O3, and platinum content is 0.2-0.4% at pressure of 1-6 MPa, temperature of 340-420°C, volume feed velocity of hydrocarbons of 0.5-1.5 h-1, the ratio of hydrogen:hydrocarbons of 800-1200:1 nl/l with further extraction by rectification from hydrocracking products of the fraction of 180°-360°C, which is subject to hydrofinishing on a palladium catalyser containing 0.5 to 1.5 wt % of palladium applied to the carrier made from γ-Al2O3 with effective pore radius of 4.0-10.0 nm; at that, hydrofinishing process is performed at the temperature of 150-250°C, pressure of 2.0-4.0 MPa, volume feed velocity of the extracted fraction of 1.0-15.0 h-1, at the ratio of hydrogen:fraction of 300-800:1 nl/l. Besides, a catalyser is described, which is used for implementation of hydrocracking/isodewaxing stage of the above method.;EFFECT: increase in yield of target fraction at improvement of catalytic activity of the catalyser.;2 cl, 1 tbl, 6 ex
机译:技术领域:一种机械;物质:描述了一种通过按照费-托法获得的固体合成碳氢化合物获得柴油燃料的方法。它涉及在含有载体和板的催化剂上对固体烃进行加氢裂化/异脱蜡;此时,载体由10-40%的沸石SAPO-41和γ-Al 2 O 3 的混合物制成,压力下铂含量为0.2-0.4% 1-6 MPa的温度,340-420°C的温度,0.5-1.5 h -1 的烃的进料速度,800:1200:1 nl / l的氢:烃比通过精馏从加氢裂化产物中进一步萃取出馏分180°-360°C,然后将其在含0.5-1.5 wt%钯的γ-Al 2载体上的钯催化剂上进行加氢精制。 Sub> O 3 ,有效孔径为4.0-10.0 nm;此时,在150-250°C的温度,2.0-4.0 MPa的压力,1.0-15.0 h -1 的萃取馏分的体积进料速度下进行加氢精制工艺。氢:300-800:1 nl / l的馏分。此外,描述了一种用于实施上述方法的加氢裂化/等脱蜡阶段的催化剂。效果:在提高催化剂催化活性的同时增加了目标馏分的收率。2 cl,1 tbl,6 ex

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